JP2012192306A - System for removing and treating sea bottom sludge - Google Patents
System for removing and treating sea bottom sludge Download PDFInfo
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- JP2012192306A JP2012192306A JP2011056167A JP2011056167A JP2012192306A JP 2012192306 A JP2012192306 A JP 2012192306A JP 2011056167 A JP2011056167 A JP 2011056167A JP 2011056167 A JP2011056167 A JP 2011056167A JP 2012192306 A JP2012192306 A JP 2012192306A
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Abstract
Description
本発明は海底汚泥の除去処理システムに関する。詳しくは、海域や海底の有機堆積表泥を効率的に除去し、更に有害物の処理及び最終処分をする海底汚泥の除去処理システムに係るものである。 The present invention relates to a seabed sludge removal treatment system. Specifically, the present invention relates to a seabed sludge removal treatment system that efficiently removes organic sedimentation surface mud from the sea area and the seabed, and further treats harmful substances and performs final disposal.
なお、ここで言う海底汚泥とは、有機スズ等の環境ホルモンが軽微な含有で、高含水比、軽比重(1.1t/m3から1.2t/m3)、かつ硫化物、有機物、全窒素、全有機炭素を高含有する海底を覆う表泥、及びその海底に定着しがたい微粒子から形成された漂泥、浮泥をいう。これらは陸上、水中を問わず存在する硫酸還元菌と反応し硫化ガスを発生、無酸素状態を惹起し、その結果健全な底生生物を激減させると共に嫌気性底生生物を増殖させ、底生生物の常に沈降する有機物消化能力を妨げることにより、更に硫化ガス発生を連発し、健全な動植物プラクトンの生育を阻害するという悪循環連鎖を及ぼすものである。 In addition, the seabed sludge referred to here has a slight content of environmental hormones such as organic tin, high water content, light specific gravity (1.1 t / m 3 to 1.2 t / m 3 ), sulfide, organic matter, Surface mud that covers the seabed with a high content of total nitrogen and total organic carbon, and mud and floating mud formed from fine particles that are difficult to settle on the seabed. These react with sulfate-reducing bacteria that exist on land and in water to generate sulfur gas, causing anoxic conditions, resulting in drastic reduction of healthy benthic organisms and proliferation of anaerobic benthic organisms. By interfering with the ability of organisms to digest organic matter that always settles, the generation of sulfur gas is further repeated, and a vicious cycle is formed in which the growth of healthy animal and plant plactones is inhibited.
近年、港湾、漁港内や養殖場等水産海域の海底に堆積した有害な海底汚泥の除去処理が求められている。
現状においては、海底汚泥表層面を健全な砂で覆う、所謂覆砂処理方法があるが、覆砂下面に有機物残存があれば、硫酸還元菌と作用して硫化ガスが発生し、発生した硫化ガスは被覆砂内部に充満し、その後表面に達する。その結果、嫌気性生物が覆砂底面から表層に移動して表層健全生物を凌駕することとなり、再び不健全化してしまう。
In recent years, there has been a demand for removal treatment of harmful seabed sludge accumulated on the seabed of marine products such as harbors, fishing ports and farms.
At present, there is a so-called sand-capping method that covers the surface of the seabed sludge with healthy sand. However, if there is organic residue on the bottom of the sand-covered sand, sulfur dioxide gas is generated by the action of sulfate-reducing bacteria. The gas fills the coated sand and then reaches the surface. As a result, the anaerobic organisms move from the sand-covered bottom surface to the surface layer, surpassing the surface healthy organisms and become unhealthy again.
ここで、海底汚泥を浚渫、あるいは吸引等によって揚陸し、陸上において浄化処理する方法として、例えば特許文献1に記載されたものが知られている。
具体的には、図6に示すように、少なくとも、海底汚泥を含有する汚泥を充填し、ビタミン類を添加して分解反応を行うための第1反応槽101と、この汚泥に酸素非含有気体を通気するための通気管102と、汚泥の上澄み液であって、汚泥の分解反応により生成する有機体を含有する上澄み液を抜き取るための送液手段103と、この上澄み液を供給し、有機酸の分解反応を行うための反応槽であって、有機酸分解能を有する微生物を含有する第2反応槽104と、有機酸の分解により発生した気体を第2反応槽104から除去する手段と、有機酸を分解した後の排出液を放出する手段を有する構成の汚泥処理装置が知られている。
Here, for example, a method described in
Specifically, as shown in FIG. 6, at least a
しかしながら、浚渫された汚泥は海岸、あるいは船上で連続的、かつ大量に処理する必要があるが、特許文献1に記載された汚泥処理装置では2個の反応槽で汚泥処理を行うために処理能力に限界がある。
However, it is necessary to treat dredged sludge continuously and in large quantities on the beach or on the ship. However, the sludge treatment apparatus described in
また、浚渫される汚泥には、土砂やフロック形成物が多く含まれており、このような高含水の汚泥を処理して海洋に廃棄することには問題がある。 In addition, sludge to be drowned contains a lot of earth and sand and floc-forming substances, and there is a problem in treating such high-water-containing sludge and disposing it in the ocean.
更に、海底汚泥は、有機スズ等の環境ホルモンや重金属などの有害物質を含まない場合や、生物環境に影響を及ぼさない程度の成分量である場合には、一般廃棄として処理しても良い。そのため、特許文献1に記載された汚泥処理装置のように、事前の汚泥成分の調査をせずに反応槽内で有機物を分解反応させて処理するのでは非常に効率が悪い。
Further, the seabed sludge may be treated as general waste when it does not contain environmental hormones such as organotin and harmful substances such as heavy metals, or when the amount of components does not affect the biological environment. Therefore, as in the sludge treatment apparatus described in
本発明は以上の点に鑑みて創案されたものであって、浚渫された汚泥の最終処分までの工程を効率良く、かつ大量に処理をすることを実現可能とする海底汚泥の除去処理システムを提供することを目的とするものである。 The present invention was devised in view of the above points, and provides a submarine sludge removal treatment system that can realize efficient and large-scale processing up to final disposal of trapped sludge. It is intended to provide.
上記の目的を達成するために、本発明に係る海底汚泥の除去処理システムは、泥水化された有機物を含む高含水比の浚渫土砂が投入される処理槽と、前記処理槽の底面に形成された溝状の排水ドレーンと、前記排水ドレーンの開口端に覆着されたろ過シートと、前記排水ドレーン以外の底面上に覆設された防水シートと、前記ろ過シート及び防水シート上に積層された砂とを備える。 In order to achieve the above object, a seabed sludge removal treatment system according to the present invention is formed on a bottom surface of a treatment tank into which dredged sand with a high water content containing muddy water is put. A groove-shaped drainage drain, a filtration sheet covered at the open end of the drainage drain, a waterproof sheet covered on the bottom surface other than the drainage drain, and laminated on the filtration sheet and the waterproof sheet. With sand.
ここで、泥水化された有機物を含む高含水比の浚渫土砂を処理槽内に投入することで、処理槽の底面に形成された溝状の排水ドレーンと、この排水ドレーンの開口端に覆着されたろ過シートと、排水ドレーン以外の底面上に覆設された防水シートと、ろ過シート及び防水シート上に積層された砂によって、土砂、フロック形成沈降堆積物と海水との分離が可能となる。そして、このことによって、海水はろ過シートを通して排水ドレーンより濁度管理の後に海域放流することができ、土砂、フロック形成沈降堆積物は脱水処理した後に廃棄処理することができる。 Here, dredged dredged sand containing organic matter that has become muddy water is put into the treatment tank, so that it covers the grooved drainage drain formed on the bottom of the treatment tank and the open end of this drainage drain. Separation of earth and sand, flock-forming sediments and seawater is possible by the filtered sheet, the waterproof sheet laid on the bottom surface other than the drainage drain, and the sand laminated on the filter sheet and the waterproof sheet. . And by this, seawater can be discharged into the sea area after the turbidity control from the drainage drain through the filter sheet, and the sediment and floc-forming sediment can be discarded after being dehydrated.
また、排水ドレーン内に砕石が充填された場合には、海水に含まれている不純物を砕石で吸着することができる。 Further, when crushed stone is filled in the drainage drain, impurities contained in seawater can be adsorbed by crushed stone.
更に、積層された砂の上に通水性の砂表面被膜シートが設けられた場合には、土砂と海水とを分離することが可能となる。 Furthermore, when a water-permeable sand surface coating sheet is provided on the laminated sand, it becomes possible to separate earth and sand from seawater.
また、排水ドレーンが底面に複数設けられた場合には、処理槽内に投入される浚渫土砂の脱水を効率良く行うことができる。 In addition, when a plurality of drainage drains are provided on the bottom surface, dredged dredged sand can be efficiently removed.
また、排水ドレーンが処理槽の外部に配置された貯留タンクに連通された場合には、排水ドレーンが海水で飽和することなく、継続した海水のろ過が可能となる。 In addition, when the drainage drain is communicated with a storage tank disposed outside the treatment tank, the drainage drain is not saturated with seawater, and continuous seawater filtration is possible.
また、ろ過シートがポリエチレン系、あるいはポリエステル系不織布から形成された場合には、分離した海水中に含まれるダイオキシン及びトリブチルスズを含む微小なフロックを除去することが可能となり濁度管理の後に海域放流をすることができる。 In addition, if the filter sheet is made of polyethylene or polyester nonwoven fabric, it is possible to remove minute flocs containing dioxin and tributyltin contained in the separated seawater, and release the sea area after turbidity control. can do.
また、処理槽内にドレーン材が配置され、このドレーン材に真空ポンプが接続された場合には、処理槽内の沈降堆積物の高含水比の土砂、フロック形成沈降堆積物を大量に、かつ効率良く脱水することができる。 In addition, when a drain material is disposed in the treatment tank and a vacuum pump is connected to the drain material, a large amount of sediment with a high water content of sediment in the treatment tank, floc-forming sedimentation deposit, and Dehydrated efficiently.
本発明の海底汚泥の除去処理システムによれば、浚渫された海底汚泥を土砂、フロック形成沈降堆積物と海水とを分離することで、浚渫された汚泥の最終処分までの工程を効率良く、かつ大量に処理をすることが実現可能となる。 According to the seabed sludge removal treatment system of the present invention, the dredged seabed sludge is separated from earth and sand, flock-forming sediments and seawater, and the process up to final disposal of the drowned sludge is efficiently performed, and A large amount of processing can be realized.
以下、本発明の実施の形態を図面を参酌しながら説明し、本発明の理解に供する。
<実施例1>
図1は本発明を適用した海底汚泥の除去処理システムの一例を説明するための平面模式図であり、図2は本発明を適用した海底汚泥の除去処理システムの一例を説明するための側面模式図である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings to provide an understanding of the present invention.
<Example 1>
FIG. 1 is a schematic plan view for explaining an example of a seabed sludge removal treatment system to which the present invention is applied, and FIG. 2 is a side view for explaining an example of a seabed sludge removal treatment system to which the present invention is applied. FIG.
ここで示す海底汚泥の除去処理システム1は、海底汚泥が収容される処理槽3と、この処理槽3の底面17に一定間隔ごとに配置された排水ドレーン4と、これらの排水ドレーン4からの排水を誘導する誘導路5と、この誘導路5からの排水を貯留する貯留タンク6とから構成されている。
The seabed sludge
ここで、処理槽3は1日の汚泥処理量(400m3)を考慮して縦、横20mの長さ及び地面より高さ70cmとされる囲繞堤2によって形成され、更に処理槽3内の底面17は地面より60cm掘り下げられて構成されている。
Here, the
また、排水ドレーン4は処理槽3の底面に一定間隔ごと配置されている。この排水ドレーン4は図3に示すように、直径が約300cmの半円筒形状の樋部7を地盤8内に埋設し、その開口端が底面17と同一面上となるような構成とされている。
Further, the
更に、樋部7内に砕石9が充填されると共に、この樋部7の開口端にポリエチレン系、あるいはポリエステル系不織布で形成されたろ過シート10が覆着されている。また、ろ過シート10が覆着された領域以外の底面17にはビニール材で形成された防水シート11が覆着されている。
Further, the crushed
ここで、ろ過シート10及び防水シート11上には約10cm厚さの脱水、ろ過用としての砂12が積層されている。
Here, on the
更に、砂12の表面にはコンマット3mmの通水性の砂表面被膜シート13が設けられている。また、それぞれの樋部7の一端側には、これらの樋部7と連通状とされた誘導路5が配置されている。
Further, a water-permeable sand
この誘導路5は、囲繞堤2の下部を貫通した状態で処理槽3外へ延設されている。なお、それぞれの誘導路5の開口端には排水路14が臨んだ状態で配置されている。
The
更に、排水路14の一端側には貯留タンク6が配置され、この貯留タンク6に貯留されるろ過水はポンプ(図示せず。)によって海等へ排水されるような構成とされている。
Furthermore, the
以上の構成よりなる本発明の海底汚泥の除去処理システムでは、図4に示すように、まず、漁港や養殖場などの海底を覆う汚泥(表泥、標泥、浮泥とも言う。)を海水と共に浚渫装置(図示せず。)によって浚渫し、浚渫された汚泥は除去泥水運搬船(図示せず。)に投入される。
なお、汚泥の深さは通常10cm程度である。
In the seabed sludge removal treatment system of the present invention having the above configuration, first, as shown in FIG. At the same time, the sludge that has been dredged by the dredger device (not shown) is thrown into a removed mud carrier (not shown).
In addition, the depth of sludge is about 10 cm normally.
次に、除去泥水運搬船に回収された汚泥は、サンドポンプ等によって陸上に設置された処理槽3内に搬送投入される。
Next, the sludge collected in the removed mud transport ship is transported and charged into the
ここで、処理槽3内に投入された汚泥Aは、水分含有率が非常に高く、砂12上に被覆された砂表面被覆シート13を通して水分のみが砂12層内に通水されることとなる。
Here, the sludge A introduced into the
この砂12層内を汚水が通過することで、汚水がろ過され、汚水に含まれる浮遊フロックが除去されることとなる。 By passing the sewage through the 12 layers of sand, the sewage is filtered and the floating floc contained in the sewage is removed.
更に、砂12層によってろ過された汚水Aは、排水ドレーン4のポリエチレン系、あるいはポリエステル系不織布で形成されたろ過シート10を通して樋部7内に通水されることとなる。
なお、樋部7以外の底面17には防水シート11が覆着されていることから、地盤に汚水が浸透せず、排水ドレーン4内にろ過シート10を通して樋部7内に通水される。
Furthermore, the sewage A filtered by the 12 layers of sand is passed through the
In addition, since the waterproof sheet 11 is covered on the bottom surface 17 other than the
ここで、ろ過シート10によってトリブチルスズ(TBT)の相当量を包含する浮遊フロックを吸着して規制値以下の濁度となるように濾過することができる。
Here, the floating floc containing a considerable amount of tributyltin (TBT) can be adsorbed by the
そして、樋部7内に通水された汚水Aは誘導路5を通り貯留タンク6に集められる。
この際に、除去海底汚泥の硫化物含有が(0.1〜0.2)mg/g、有機物含有が8%超で10%以下、DXNが(150〜1000)pg−TEQ/g−dry、TBTが(300〜1000)ng/gである場合には、濾過水の濁度が2程度以下となるまで濾過をした後に放流する。
Then, the sewage A that has passed through the
At this time, the removed seabed sludge contained sulfide (0.1 to 0.2) mg / g, the organic matter contained more than 8% and 10% or less, and DXN was (150 to 1000) pg-TEQ / g-dry. When TBT is (300 to 1000) ng / g, it is discharged after filtering until the turbidity of filtered water is about 2 or less.
また、除去海底汚泥に含まれる硫化物が0.3mg/g超、有機物10%超、DXN(1000〜6000)pg−TEQ/g−dry、TBT1000ng/g超である場合には、濁度が0〜1程度以下となるまで濾過をした後に放流する。 Moreover, when the sulfide contained in the removed seabed sludge is more than 0.3 mg / g, more than 10% organic matter, DXN (1000 to 6000) pg-TEQ / g-dry, TBT more than 1000 ng / g, the turbidity is It discharges, after filtering until it becomes about 0-1 or less.
また、脱水した沈降泥は乾燥場に搬送し、バックフォー等の重機によって耕耘(沈降脱水泥の天地変転)を行い、大気接触、自然乾燥即ち好気性処理を促し、硫化物、有機物の酸化を図り無害化する。
なお、有機物が多い場合、天日乾燥効果が悪い気象状況次第では次亜塩素酸カルシウム、生石灰等を散布し悪臭発生化合物の酸化を促進し対応する。
In addition, dewatered sedimented mud is transported to a dry field and plowed by heavy machinery such as backhoe (transformation of sedimented dewatered mud) to promote atmospheric contact, natural drying, that is, aerobic treatment, and oxidation of sulfides and organic matter. Detoxify.
If there is a lot of organic matter, depending on the weather conditions where the sun drying effect is bad, calcium hypochlorite, quicklime, etc. are sprayed to promote the oxidation of the malodorous compound.
本発明の海底汚泥の除去処理システムでは、処理水中に含まれる有害物質の事前測定を行い、この測定値に基づいて濁度の目標値を定め、多重不織布により設定濁度以下に濾過した後に海域に放流することによって、無害化処理が可能となる。 In the seabed sludge removal treatment system of the present invention, the pre-measurement of harmful substances contained in the treated water is performed, the target value of turbidity is determined based on this measured value, and the sea area is filtered after being set below the set turbidity by multiple nonwoven fabrics. The detoxification process becomes possible by discharging it into the water.
また、固液分離された高含水の沈降泥は脱水、減容化された後に好気性措置で無害化処理されることによって、小規模設備による工程の短縮と効率の良い海底汚泥の処理が可能となる。 In addition, the high-water sedimented sludge separated from solid and liquid can be detoxified by aerobic measures after dehydration and volume reduction. It becomes.
更に、土砂及びフロック沈降堆積物と海水を分離した後に、硫化物酸化剤及び有機物酸化剤を添加して混合することによって、有機物が多い場合、あるいは天候不良で天日乾燥効果が悪い状況下では次亜塩素酸カルシウム、石灰等の硫化物酸化剤及び有機物酸化剤を散布し、悪臭発生化合物の酸化の促進を可能とする。 Furthermore, after separating the sediment and floc sediment and seawater, adding sulfide oxidizer and organic oxidizer and mixing them, when there is a lot of organic matter, or under the bad weather drying effect due to bad weather It is possible to promote the oxidation of malodorous compounds by spraying sulfide oxidants such as calcium hypochlorite and lime and organic oxidants.
なお、ダイオキシン類の環境濃度を表わす単位としてのpg−TEQ/g−dryは、この単位の「p(ピコ)」は、pico―(=一兆分の1)の意を表す接頭語の略で、「TEQ」は毒性当量を表す。
また、ダイオキシン類は、同じ量(ピコグラム数)でも種類(塩素原子の置換位置・数:右の構造式で5と10を除く全ての位置に水素原子に換わって塩素原子が入る事ができる)によって毒性が大きく異なる。このために、毒性(環境に与える影響)を評価するときは、ダイオキシン類の中で最も毒性に強い、右の構造を持った2、3、7,8−tetrachloro dibenzo―p−dioxin:2、3、7、8―四塩化ジベンゾーバラージオキシン)の毒性を1として他のダイオキシンの毒性の強さを換算して評価している。
Note that pg-TEQ / g-dry as a unit representing the environmental concentration of dioxins is “p (pico)”, which is an abbreviation of a prefix representing pico-(= one trillionth). "TEQ" represents a toxic equivalent.
In addition, dioxins are of the same amount (picogram number) and are of the same type (chlorine atom substitution position / number: chlorine atoms can be substituted for hydrogen atoms at all positions except 5 and 10 in the right structural formula) Toxicity varies greatly depending on. Therefore, when evaluating toxicity (effect on the environment), 2, 3, 7, 8-tetrachloro dibenzo-p-dioxin having the right structure, which is the most toxic among dioxins, 2, (3,7,8-dibenzo-baradioxin tetrachloride) is assumed to be 1, and the toxicity intensity of other dioxins is converted and evaluated.
<実施例2>
図5は本発明を適用した海底汚泥の除去処理システムにおける処理槽の一例を説明するための模式図である。
<Example 2>
FIG. 5 is a schematic diagram for explaining an example of a treatment tank in a seabed sludge removal treatment system to which the present invention is applied.
ここで示す海底汚泥の除去処理システム1Aは、前記図1において詳述するように、海底汚泥が収容される処理槽3と、この処理槽3の底面17に一定間隔ごとに配置された排水ドレーン4と、これらの排水ドレーン4からの排水を誘導する誘導路5と、この誘導路5からの排水を貯留する貯留タンク6とから構成されている。
As shown in detail in FIG. 1, the seabed sludge
ここで、処理槽3は1日の汚泥処理量(400m3)を考慮して縦、横20mの長さ及び地面より高さ70cmとされる囲繞堤2によって形成され、更に処理槽3内の底面17は地面より60cm掘り下げられて構成されている。
Here, the
また、排水ドレーン4は処理槽3の底面に一定間隔ごと配置されている。この排水ドレーン4は図3に示すように、直径が約20〜30cmの半円筒形状の樋部7を地盤8内に埋設し、その開口端が底面17と同一面上となるような構成とされている。
Further, the
この樋部7内に砕石9が充填されると共に、その開口端にポリエチレン系、あるいはポリエステル系不織布で形成されたろ過シート10が覆着されている。また、ろ過シート10が覆着された領域以外の底面17にはビニール材で形成された防水シート11が覆着されている。
The crushed portion 9 is filled with the crushed stone 9, and a
ここで、ろ過シート10及び防水シート11上には約10cm厚さの脱水、ろ過用としての砂12が積層され、その表面にはコンマット3mmの通水性の砂表面被膜シート13が設けられている。
Here, a
また、それぞれの樋部7の一端側には、これらの樋部7と連通状とされた誘導路5が配置されると共に、囲繞堤2の下部を貫通した状態で処理槽3外へ延設されている。なお、それぞれの誘導路5の開口端には排水路14が臨んだ状態で配置されている。
In addition, on one end side of each
更に、排水路14の一端側には貯留タンク6が配置され、この貯留タンク6に貯留されるろ過水はポンプ(図示せず。)によって海等へ排水されるような構成とされている。
Furthermore, the
ここで、処理槽3内にドレーン材15が配置され、このドレーン材15に真空ポンプ16が接続されて構成されている。
Here, a drain material 15 is disposed in the
以上の構成よりなる本発明の海底汚泥の除去処理システムでは、漁港や養殖場などの海底を覆う汚泥(表泥、標泥、浮泥とも言う。)を海水と共に浚渫装置(図示せず。)によって浚渫し、浚渫された汚泥は除去泥水運搬船(図示せず。)に投入される。
なお、汚泥の深さは通常10cm程度である。
In the seabed sludge removal treatment system of the present invention having the above-described configuration, sludge (also referred to as surface mud, sewage mud, and floating mud) that covers the sea bottom of a fishing port, aquaculture farm, or the like is dredged with seawater (not shown). The sludge that has been dredged is put into a removed mud carrier (not shown).
In addition, the depth of sludge is about 10 cm normally.
更に、除去泥水運搬船に回収された汚泥は、サンドポンプ等によって陸上に設置された処理槽3内に搬送投入される。
Furthermore, the sludge collected by the removed mud transport ship is transported into the
この処理槽3内に投入された汚泥Aは、水分含有率が非常に高く、ドレーン材15に接続した真空ポンプ16吸引で水を吸引し、そうすることで汚泥Aを圧密状態とし圧密沈下させる。
The sludge A introduced into the
また、汚泥A内の汚水は砂12層内を通過することで、汚水がろ過され、汚水に含まれる浮遊フロックが除去されることとなる。
In addition, the sewage in the sludge A passes through the
更に、砂12層によってろ過された汚水Aは、排水ドレーン4のポリエチレン系、あるいはポリエステル系不織布で形成されたろ過シート10を通して樋部7内に通水されることとなる。
なお、樋部7以外の底面17には防水シート11が覆着されていることから、地盤に汚水が浸透せず、排水ドレーン4内にろ過シート10を通して樋部7内に通水される。
Furthermore, the sewage A filtered by the 12 layers of sand is passed through the
In addition, since the waterproof sheet 11 is covered on the bottom surface 17 other than the
また、汚泥A表面に滲み出た滲出水Bとドレーン材15より吸引された水は、貯留タンク(図示せず。)に貯水される。ここで、ろ過速度を調整した上でリエチレン系、あるいはポリエステル系不織布で形成された多重不織布濾過槽(図示せず。)を通じ、濁度が2以下であることを確認した上で、海域に放流する。 Further, the exuded water B that has exuded on the surface of the sludge A and the water sucked from the drain material 15 are stored in a storage tank (not shown). Here, after adjusting the filtration speed, it was confirmed that the turbidity was 2 or less through a multiple non-woven fabric filtration tank (not shown) formed of a polyethylene-based or polyester-based non-woven fabric, and then released into the sea area. To do.
また、脱水した沈降泥はバックフォー等の重機によって耕耘(沈降泥の天地変転)を行い、大気接触、自然乾燥を促し、硫化物、有機物の酸化を計り安定化した後に、一般廃棄物処理場で最終地層処分する。
なお、有機物が多い場合、天日乾燥効果が悪い気象状況次第では次亜塩素酸カルシウム、石灰等を散布し悪臭発生化合物の酸化を促進し対応する。
In addition, dewatered sedimented mud is cultivated by heavy machinery such as backhoes (transformation of sedimented mud upside down), promotes air contact and natural drying, measures and stabilizes oxidation of sulfides and organic matter, and then stabilizes it at a general waste treatment plant. At the final geological disposal.
If there is a lot of organic matter, depending on the weather conditions where the sun drying effect is bad, calcium hypochlorite, lime, etc. are sprayed to promote the oxidation of the malodor generating compound.
本発明の海底汚泥の除去処理システムでは、除去底質に含まれる有機物質の固液分離後の事前予測測定を行い、海域に影響を及ぼさない濁度管理を行い、確認した上で、海域放流が可能となる。 In the seabed sludge removal treatment system of the present invention, preliminary prediction measurement after solid-liquid separation of organic substances contained in the removed sediment is performed, and turbidity management that does not affect the sea area is performed and confirmed, and then released into the sea area. Is possible.
また、フロック沈降堆積物の脱水は、同フロック沈降堆積物底面にドレーン材を配置し、自然脱水を行うことによって、高含水比の土砂、フロック形成沈降堆積物を大量に、かつ効率良く脱水することが可能となる。 In addition, dehydration of floc sedimentation sediments is carried out by placing drain material on the bottom of the floc sedimentation sediment and performing natural dehydration, thereby dewatering large amounts of sediment with high water content and floc sedimentation sediments efficiently. It becomes possible.
また、固液分離された高含水の沈降泥は脱水、減容化された後に自然乾燥され、無害化あるいは、安定化によって、比較的確保可能な一般廃棄物処分施設での処理が可能となる。 In addition, the high-moisture sedimented mud that has been separated into solid and liquid is dehydrated and volume-reduced, and then air-dried, making it harmless or stable, so that it can be processed in a relatively secure general waste disposal facility. .
これにより、臨海部、土砂処理処分場の不足現状に鑑み、地層処分後ガスの発生、あるいは含有物流出等の事態が生じないように脱水、減容化、好気性誘導を同時並行的に簡便な装置をもって行い、処理泥の大幅な減容化、同搬出作業の容易化及び安定化、無害化処理を可能とする。 As a result, in view of the shortage of coastal areas and sediment disposal sites, dehydration, volume reduction, and aerobic induction can be easily performed in parallel to prevent gas generation after geological disposal or outflow of contents. It is possible to reduce the volume of treated mud, facilitate and stabilize the unloading work, and make it harmless.
1、1A 海底汚泥の除去処理システム
2 囲繞堤
3 処理槽
4 排水ドレーン
5 誘導路
6 貯留タンク
7 樋部
8 地盤
9 砕石
10 ろ過シート
11 防水シート
12 砂
13 砂表面被膜シート
14 排水路
15 ドレーン材
16 真空ポンプ
17 底面
DESCRIPTION OF
Claims (7)
前記処理槽の底面に形成された溝状の排水ドレーンと、
前記排水ドレーンの開口端に覆着されたろ過シートと、
前記排水ドレーン以外の底面上に覆設された防水シートと、
前記ろ過シート及び防水シート上に積層された砂とを備える
海水汚泥の除去処理システム。 A treatment tank into which dredged soil with a high water content containing muddy water is placed;
A grooved drainage drain formed on the bottom surface of the treatment tank;
A filtration sheet coated on the open end of the drainage drain;
A waterproof sheet laid on the bottom surface other than the drainage drain;
A seawater sludge removal treatment system comprising the filtration sheet and sand laminated on the waterproof sheet.
請求項1に記載の海水汚泥の除去処理システム。 The seawater sludge removal treatment system according to claim 1, wherein crushed stone is filled in the drainage drain.
請求項1または請求項2に記載の海水汚泥の除去処理システム。 The seawater sludge removal treatment system according to claim 1, wherein a water-permeable sand surface coating sheet is provided on the laminated sand.
請求項1、請求項2または請求項3に記載の海水汚泥の除去処理システム。 The seawater sludge removal treatment system according to claim 1, wherein a plurality of the drainage drains are provided on the bottom surface.
請求項1、請求項2、請求項3または請求項4に記載の海水汚泥の除去処理システム。 The seawater sludge removal treatment system according to claim 1, 2, 3, or 4, wherein the drainage drain is communicated with a storage tank disposed outside the treatment tank.
請求項1、請求項2、請求項3または請求項4に記載の海水汚泥の除去処理システム。 The seawater sludge removal treatment system according to claim 1, wherein the filtration sheet is formed from a polyethylene-based or polyester-based nonwoven fabric.
請求項1、請求項2、請求項3、請求項4、請求項5または請求項6に記載の海水汚泥の除去処理システム。 The drain material is arrange | positioned in the said processing tank, and the vacuum pump was connected to this drain material. The seawater sludge of Claim 1, Claim 2, Claim 3, Claim 5 or Claim 6 Removal processing system.
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